EP1255535A2 - Controlled release pharmaceutical composition containing tramadol hydrochloride - Google Patents

Controlled release pharmaceutical composition containing tramadol hydrochloride

Info

Publication number
EP1255535A2
EP1255535A2 EP00987947A EP00987947A EP1255535A2 EP 1255535 A2 EP1255535 A2 EP 1255535A2 EP 00987947 A EP00987947 A EP 00987947A EP 00987947 A EP00987947 A EP 00987947A EP 1255535 A2 EP1255535 A2 EP 1255535A2
Authority
EP
European Patent Office
Prior art keywords
weight
pharmaceutical composition
amount
controlled release
fatty acids
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP00987947A
Other languages
German (de)
French (fr)
Other versions
EP1255535B1 (en
Inventor
L'uboslav Razus
Helena Sedlarov
Ivan Varga
Ondrej Gattnar
Marián ZEMaNEK
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zentiva KS
Original Assignee
Slovakofarma AS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Slovakofarma AS filed Critical Slovakofarma AS
Priority to SI200030873T priority Critical patent/SI1255535T1/en
Publication of EP1255535A2 publication Critical patent/EP1255535A2/en
Application granted granted Critical
Publication of EP1255535B1 publication Critical patent/EP1255535B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/20—Pills, tablets, discs, rods
    • A61K9/2004—Excipients; Inactive ingredients
    • A61K9/2022—Organic macromolecular compounds
    • A61K9/2027—Organic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/13—Amines
    • A61K31/135—Amines having aromatic rings, e.g. ketamine, nortriptyline
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/20—Pills, tablets, discs, rods
    • A61K9/2004—Excipients; Inactive ingredients
    • A61K9/2009—Inorganic compounds
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/20—Pills, tablets, discs, rods
    • A61K9/2004—Excipients; Inactive ingredients
    • A61K9/2013—Organic compounds, e.g. phospholipids, fats
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P25/00—Drugs for disorders of the nervous system
    • A61P25/04—Centrally acting analgesics, e.g. opioids
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]

Definitions

  • Controlled release pharmaceutical composition containing tramadol hydrochloride and method for its preparation
  • the invention belongs to the pharmaceutical field, it relates to the composition and the method of preparing of an oral therapeutic preparation in the form of controlled release tablets containing the active ingredient tramadol hydrochloride.
  • Tramadol hydrochloride containing therapeutic compositions in the form of controlled release tablets are described in SK patent No. 280496, according to which a formulation is prepared by melting a mixture of the drug and a hydrophobic or hydrophilic carrier in high performance homogenization devices with heating and cooling facilities. The molten, homogenized mixture is cooled down; particle size of the agglomerates is adjusted while undercooling the mixture in order to obtain desirable physical parameters for mechanic dividing and adjustment of the particle size for further processing.
  • the meltable carriers include, e.g., waxes, hydrogenated vegetable oils and higher fatty acid esters with glycerol.
  • Document EP 0 624 366 A1 describes a formulation containing 50-800 mg tramadol, i.e. controlled release tablets, which are produced in a similar manner, or in the form of film coated spheres (agglomerates).
  • This invention overcomes said drawbacks by a new, simpler, and low time and energy consuming method of preparing tablets containing 100 to 200 mg tramadol hydrochloride, not requiring special production equipment. Manufacture in the below described manner is practicable in pharmaceutical plants without need of one- purpose equipment.
  • the tablets made by the method of the invention fulfil the requirements for the release pattern and do not require any further finish by, e.g. film coating, which would influence the release rate.
  • the principle of the manufacture is a balanced mixture of the drug and the adjuvants, prepared by simple granulation, drying of the granulate, admixing further adjuvants facilitating the tabletting process without need of further treatment of the compressed articles.
  • obtained tablets are physically and chemically stable, easily adjustable and ensure necessary optimal course of release of the active substance into the organism over the required time period even after possible dividing of the tablets.
  • the controlled release formulation according to this invention contains other adjuvants in addition to the active substance: a) Micronized esters of glycerol with higher fatty acids, preferably docosanoic acid glyceryl ester. They are of a particle size from 1 to 100 micrometers, preferably of a distribution the size of which is 1.5-60 micrometers in the range of 90 %. It has been determined experimentally in laboratory development that the most preferred content of the higher fatty acid glyceryl esters for the targeted drug release and optimal physical characteristics is from 10 to 53 % by weight, preferably, from 28 to 47 % by weight.
  • phosphoric acid preferably calcium phosphate dihydrate
  • Pharmaceutically applicable alkali salts of phosphoric acid preferably calcium phosphate dihydrate, in amounts of from 20 to 41 % by weight, preferably from 24 to 39 % by weight.
  • Non-ionic polymers of vinylpyrrolidone of relative molecular weight from 9000 to 90000, preferably 25000 to 30000, in ar ⁇ ou its from 1.15 to 1.75 % by weight, preferably from 1.3 to 1.55 % by weight.
  • alkaline earth metals preferably magnesium stearate
  • silicon dioxide preferably colloidal silica
  • the manufacturing process of this invention consists in mixing the active substance in admixture with micronized higher fatty acid glycerol ester, preferably with glyceryl ester of docosanoic acid having a particle size of from 1 - 100 micrometers, preferably 1.5 - 60 micrometers, in an amount of from 10 % to 53 % by weight, preferably from 28 % to 47 % by weight, along with alkali salts of phosphoric acid, preferably calcium phosphate dihydrate, in an amount of from 20 % to 41 % by weight, preferably from 24 % to 39 % by weight.
  • This mixture is moistened with a solution of a non-ionic vinylpyrrolidone polymer having a relative molecular weight of from 9,000 to 90,000, preferably from 25,000 to 30,000, in an amount of 1.15 to 1.75 % by weight, preferably from 1.3 to 1.55 % by weight, in a mixture of water and ethyl alcohol in an amount of from 30 % to 70 % by weight, preferably from 40 % to 60 % by weight.
  • a non-ionic vinylpyrrolidone polymer having a relative molecular weight of from 9,000 to 90,000, preferably from 25,000 to 30,000, in an amount of 1.15 to 1.75 % by weight, preferably from 1.3 to 1.55 % by weight, in a mixture of water and ethyl alcohol in an amount of from 30 % to 70 % by weight, preferably from 40 % to 60 % by weight.
  • the mixture is agitated while agglomerating.
  • the obtained agglomerate is dried in a suitable manner either by fluidisation, in a chamber or in vacuo such that the mixture contain from 0.2-1.5 %, preferably from 0.5 to 1.2 % moisture.
  • the dried agglomerate is adjusted to a particle size that complies with the tabletting process, and materials from the group of salts of higher fatty acids with alkaline earth metals, preferably magnesium stearate, in an amount of from 1.5 % to 3.2 % by weight, preferably from 1.8 % to 2.8 % by weight, and of silicon oxides, preferably colloidal silica, in an amount of from 1 % to 1.3 % by weight, preferably from 1.1 % to 2.1 % by weight, are added.
  • alkaline earth metals preferably magnesium stearate
  • the mixture is agitated until homogeneous.
  • the mixture is tabletted, the break resistance of tablets ranging from 40 to 110 N, preferably from 50 to 90 N, for tablets of round, lenticular, oblong or other shapes.
  • prepared tablets can be adjusted into commonly useful types of packages such as glass, plastics, metal packages and combinations thereof.
  • Colloidal silica 0.0060 g 1.30 %
  • the active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1.5 - 60 micrometers in the amount of 36.96 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 38.48 % by weight, for 3 minutes.
  • a suitable type of pharmaceutical granulator such as Diosna
  • the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.52 % by weight in 60% ethanol.
  • the mixture is agitated, agglomerate thus being formed.
  • the prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
  • a fluidising drying device such as Glatt or Aeromatic
  • the particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt.
  • the adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.3% by weight is added and agitated until homogeneous.
  • the obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into round- shaped, biconvex tablets.
  • Example 2 a) pharmaceutical composition, containing in 1 tablet:
  • Colloidal silica 0.0090 g 1.30 % b) process for its preparation The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1 5 - 60 micrometers in the amount of 36 96 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 38 48 % by weight, for 3 minutes
  • the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1 52 % by weight in 60% ethanol
  • the mixture is agitated, agglomerate thus being formed
  • the prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C At that point the product reaches residual moisture from 0 5 % to 1 2 %
  • the particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1 30 mm on an oscillating device such as Frewitt
  • the adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1 30% by weight is added and agitated until homogeneous
  • the obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc into round- shaped, flat tablets with dividing groove
  • the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.37 % by weight in 60% ethanol.
  • the mixture is agitated, agglomerate thus being formed.
  • the prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
  • a fluidising drying device such as Glatt or Aeromatic
  • the particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt.
  • the adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.18% by weight is added and agitated until homogeneous.
  • the obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into round-shaped, flat tablets with dividing groove.
  • the active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size ol from 1.5 - 60 micrometers in the amount of 45.64 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 24.16 % by weight, for 3 minutes.
  • the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.34 % by weight in 60% ethanol.
  • the mixture is agitated, agglomerate thus being formed.
  • the prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
  • a fluidising drying device such as Glatt or Aeromatic
  • the particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt.
  • the adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, magnesium stearate in the amount of 2.01 % by weight is added and agitated until homogeneous.
  • the obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into smooth, flat tablets with dividing groove.
  • Colloidal silica 0.0120 g 1.30 %
  • the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.52 % by weight in 60% ethanol.
  • the mixture is agitated, agglomerate thus being formed.
  • the prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 C C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
  • a fluidising drying device such as Glatt or Aeromatic
  • the particle size of the dried agglomerate is adjusted 'Dy passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt.
  • the adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.30% by weight is added and agitated until homogeneous.
  • the obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into flat, oblong tablets with dividing groove.
  • the invention can be employed in the pharmaceutical industry in obtaining controlled release therapeutic preparations, containing tramadol hydrochloride.
  • Said preparations are indicated in therapy of acute and chronic moderate to strong pain of various origins, in particular in surgery, obstetrics, oncology, rheumatology, orthopaedics, after stomatological operations, in neurology and other fields. It is useful also for pain in ischaemic diseases (such as in myocardial infarction and in leg ischaemias).

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Abstract

The invention solves a controlled release pharmaceutical composition containing tramadol hydrochloride, characterized in that it contains 100 to 200 mg of the active ingredient in admixture with micronized esters of glycerol with higher fatty acids, alkali salts of phosphoric acid, non-ionic vinylpyrrolidone polymers, substances from the group of salts of higher fatty acids with alkaline earth metals and silicon oxides and a method for the preparation of this composition.

Description

Controlled release pharmaceutical composition containing tramadol hydrochloride and method for its preparation
Technical Field
The invention belongs to the pharmaceutical field, it relates to the composition and the method of preparing of an oral therapeutic preparation in the form of controlled release tablets containing the active ingredient tramadol hydrochloride.
Background art
Tramadol hydrochloride containing therapeutic compositions in the form of controlled release tablets are described in SK patent No. 280496, according to which a formulation is prepared by melting a mixture of the drug and a hydrophobic or hydrophilic carrier in high performance homogenization devices with heating and cooling facilities. The molten, homogenized mixture is cooled down; particle size of the agglomerates is adjusted while undercooling the mixture in order to obtain desirable physical parameters for mechanic dividing and adjustment of the particle size for further processing.
As described in SK patent No. 280496, the meltable carriers include, e.g., waxes, hydrogenated vegetable oils and higher fatty acid esters with glycerol.
Document EP 0 624 366 A1 describes a formulation containing 50-800 mg tramadol, i.e. controlled release tablets, which are produced in a similar manner, or in the form of film coated spheres (agglomerates).
Drawbacks of the above preparation of solid formulations containing tramadol hydrochloride based on meltable hydrophobic or hydrophilic carrier include, in addition to energy and time consumption, necessity of special equipment. Another drawback is the surface finish of the tablets, which requires further special equipment and technology, and dividing of the tablets for dosage is not possible. Disclosure of the Invention
This invention overcomes said drawbacks by a new, simpler, and low time and energy consuming method of preparing tablets containing 100 to 200 mg tramadol hydrochloride, not requiring special production equipment. Manufacture in the below described manner is practicable in pharmaceutical plants without need of one- purpose equipment.
The tablets made by the method of the invention fulfil the requirements for the release pattern and do not require any further finish by, e.g. film coating, which would influence the release rate.
The principle of the manufacture is a balanced mixture of the drug and the adjuvants, prepared by simple granulation, drying of the granulate, admixing further adjuvants facilitating the tabletting process without need of further treatment of the compressed articles. Thus obtained tablets are physically and chemically stable, easily adjustable and ensure necessary optimal course of release of the active substance into the organism over the required time period even after possible dividing of the tablets.
The controlled release formulation according to this invention contains other adjuvants in addition to the active substance: a) Micronized esters of glycerol with higher fatty acids, preferably docosanoic acid glyceryl ester. They are of a particle size from 1 to 100 micrometers, preferably of a distribution the size of which is 1.5-60 micrometers in the range of 90 %. It has been determined experimentally in laboratory development that the most preferred content of the higher fatty acid glyceryl esters for the targeted drug release and optimal physical characteristics is from 10 to 53 % by weight, preferably, from 28 to 47 % by weight. b) Pharmaceutically applicable alkali salts of phosphoric acid, preferably calcium phosphate dihydrate, in amounts of from 20 to 41 % by weight, preferably from 24 to 39 % by weight. c) Non-ionic polymers of vinylpyrrolidone of relative molecular weight from 9000 to 90000, preferably 25000 to 30000, in arπou its from 1.15 to 1.75 % by weight, preferably from 1.3 to 1.55 % by weight. d) Substances facilitating tabletting process from the group of salts of higher fatty acids with alkaline earth metals, preferably magnesium stearate, in amounts of 1.5 to 3.2 % by weight, preferably from 1.8 to 2.8 % by weight, and silicon dioxide, preferably colloidal silica, in amounts of from 1 to 3 % by weight, preferably from 1.1 to 2.1 % by weight.
The manufacturing process of this invention consists in mixing the active substance in admixture with micronized higher fatty acid glycerol ester, preferably with glyceryl ester of docosanoic acid having a particle size of from 1 - 100 micrometers, preferably 1.5 - 60 micrometers, in an amount of from 10 % to 53 % by weight, preferably from 28 % to 47 % by weight, along with alkali salts of phosphoric acid, preferably calcium phosphate dihydrate, in an amount of from 20 % to 41 % by weight, preferably from 24 % to 39 % by weight. This mixture is moistened with a solution of a non-ionic vinylpyrrolidone polymer having a relative molecular weight of from 9,000 to 90,000, preferably from 25,000 to 30,000, in an amount of 1.15 to 1.75 % by weight, preferably from 1.3 to 1.55 % by weight, in a mixture of water and ethyl alcohol in an amount of from 30 % to 70 % by weight, preferably from 40 % to 60 % by weight.
The mixture is agitated while agglomerating. The obtained agglomerate is dried in a suitable manner either by fluidisation, in a chamber or in vacuo such that the mixture contain from 0.2-1.5 %, preferably from 0.5 to 1.2 % moisture.
The dried agglomerate is adjusted to a particle size that complies with the tabletting process, and materials from the group of salts of higher fatty acids with alkaline earth metals, preferably magnesium stearate, in an amount of from 1.5 % to 3.2 % by weight, preferably from 1.8 % to 2.8 % by weight, and of silicon oxides, preferably colloidal silica, in an amount of from 1 % to 1.3 % by weight, preferably from 1.1 % to 2.1 % by weight, are added.
The mixture is agitated until homogeneous.
The mixture is tabletted, the break resistance of tablets ranging from 40 to 110 N, preferably from 50 to 90 N, for tablets of round, lenticular, oblong or other shapes. Thus prepared tablets can be adjusted into commonly useful types of packages such as glass, plastics, metal packages and combinations thereof.
Examples
The following examples are intended to illustrate the invention without limiting its scope.
Example 1 a) pharmaceutical composition, containing in 1 tablet:
Tramadol hydrochloride 0.1000 g 21.74 %
Glyceryl ester of docosanoic acid 0.1700 g 36.96 %
Calcium phosphate dihydrate 0.1770 g 38.48 %
Polyvinylpyrrolidone 0.0070 g 1.52 %
Colloidal silica 0.0060 g 1.30 %
b) process for its preparation:
The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1.5 - 60 micrometers in the amount of 36.96 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 38.48 % by weight, for 3 minutes.
Then the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.52 % by weight in 60% ethanol.
The mixture is agitated, agglomerate thus being formed.
The prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
The particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt. The adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.3% by weight is added and agitated until homogeneous. The obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into round- shaped, biconvex tablets.
Tablet parameters:
Dissolution of the active ingredient according to this invention as a function of time and its comparison with the product according to EP 0 624 366 A1 :
Apparatus Pharmatest type PTWS 3:
Example 2 a) pharmaceutical composition, containing in 1 tablet:
Tramadol hydrochloride 0.1500 g 21.74 %
Glyceryl ester of docosanoic acid 0.2550 g 36.96 %
Calcium phosphate dihydrate 0.2655 g 38.48 %
Polyvinylpyrrolidone 0.0105 g 1.52 %
Colloidal silica 0.0090 g 1.30 % b) process for its preparation The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1 5 - 60 micrometers in the amount of 36 96 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 38 48 % by weight, for 3 minutes
Then the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1 52 % by weight in 60% ethanol The mixture is agitated, agglomerate thus being formed
The prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C At that point the product reaches residual moisture from 0 5 % to 1 2 %
The particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1 30 mm on an oscillating device such as Frewitt The adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1 30% by weight is added and agitated until homogeneous The obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc into round- shaped, flat tablets with dividing groove
Tablet parameters
Dissolution of the active ingredient according to this invention as a function of time and its comparison with the product according to EP 0 624 366 A1 Apparatus Pharmatest type PTWS 3:
Example 3 a) pharmaceutical composition, containing in 1 tablet:
Tramadol hydrochloride 0.1500 g 29.41 %
Glyceryl ester of docosanoic acid 0.1700 g 33.33 %
Calcium phosphate dihydrate 0.1770 g 34.71 %
Polyvinylpyrrolidone 0.0070 g 1.37 %
Colloidal silica 0.0060 g 1.18 %
b) process for its preparation: The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1.5 - 60 micrometers in the amount of 33.33 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 34.71 % by weight, for 3 minutes.
Then the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.37 % by weight in 60% ethanol. The mixture is agitated, agglomerate thus being formed.
The prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
The particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt. The adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.18% by weight is added and agitated until homogeneous.
The obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into round-shaped, flat tablets with dividing groove.
Tablet parameters:
Dissolution of the active ingredient according to this invention as a function of time and its comparison with the product according to EP 0 624 366 A1.
Apparatus Pharmatest type PTWS 3:
Example 4 a) pharmaceutical composition, containing in 1 tablet:
Tramadol hydrochloride 0.2000 g 26.85 %
Glyceryl ester of docosanoic acid 0.3400 g 45.64 %
Calcium phosphate dihydrate 0.1800 g 24.16 %
Polyvinylpyrrolidone 0.0100 g 1.34 %
Magnesium stearate 0.0150 g 2.010 % b) process for its preparation: The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size ol from 1.5 - 60 micrometers in the amount of 45.64 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 24.16 % by weight, for 3 minutes.
Then the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.34 % by weight in 60% ethanol. The mixture is agitated, agglomerate thus being formed.
The prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 °C until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
The particle size of the dried agglomerate is adjusted by passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt. The adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, magnesium stearate in the amount of 2.01 % by weight is added and agitated until homogeneous. The obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into smooth, flat tablets with dividing groove.
Tablet parameters:
Dissolution of the active ingredient according to this invention as a function of time and its comparison with the product according to EP 0 624 366 A1 : Apparatus Pharmatest type PTWS 3:
Example 5 a) pharmaceutical composition, containing in 1 tablet:
Tramadol hydrochloride 0.2000 g 21.74 %
Glyceryl ester of docosanoic acid 0.3400 g 36.96 %
Calcium phosphate dihydrate 0.3540 g 38.48 %
Polyvinylpyrrolidone 0.0140 g 1.52 %
Colloidal silica 0.0120 g 1.30 %
b) process for its preparation: The active ingredient in admixture with micronized ester of glycerol with docosanoic acid having the particle size of from 1.5 - 60 micrometers in the amount of 36.9 % by weight is agitated in a suitable type of pharmaceutical granulator such as Diosna, along with calcium phosphate dihydrate in the amount of 38.48 % by weight, for 3 minutes.
Then the mixture is, under constant agitation, moistened with a solution of non-ionic vinylpyrrolidone polymer having the relative molecular weight of 25,000 in the amount of 1.52 % by weight in 60% ethanol. The mixture is agitated, agglomerate thus being formed.
The prepared agglomerate is discharged from the granulator into the vessel of a fluidising drying device such as Glatt or Aeromatic and is dried at the temperature of fed air 55 CC until the temperature of the effluent air reaches 42 °C. At that point the product reaches residual moisture from 0.5 % to 1.2 %.
The particle size of the dried agglomerate is adjusted 'Dy passing through a screen having the mesh side of 1.25 mm on an oscillating device such as Frewitt. The adjusted agglomerate is transferred into a suitable type of pharmaceutical homogenizer of the shape of cube or bulb, colloidal silica in the amount of 1.30% by weight is added and agitated until homogeneous.
The obtained mixture is tabletted in rotary tabletting machines of the type such as Manesty, Kilian, Fette etc. into flat, oblong tablets with dividing groove.
Tablet parameters:
Dissolution of the active ingredient according to this invention as a function of time and its comparison with the product according to EP 0 624 366 A1:
Apparatus Pharmatest type PTWS 3:
Industrial Applicability
The invention can be employed in the pharmaceutical industry in obtaining controlled release therapeutic preparations, containing tramadol hydrochloride. Said preparations are indicated in therapy of acute and chronic moderate to strong pain of various origins, in particular in surgery, obstetrics, oncology, rheumatology, orthopaedics, after stomatological operations, in neurology and other fields. It is useful also for pain in ischaemic diseases (such as in myocardial infarction and in leg ischaemias).

Claims

C L A I M S
1. A controlled release pharmaceutical composition containing tramadol hydrochloride characterized in that it contains 100 to 200 mg of the active ingredient in admixture with micronized esters of glycerol with higher fatty acids, alkali salts of phosphoric acid, non-ionic vinylpyrrolidone polymers, substances from the group of salts of higher fatty acids with alkaline earth metals and silicon oxides.
2. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 1 characterized in that it contains micronized esters of glycerol with higher fatty acids, preferably the glyceryl ester of docosanoic acid.
3. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 2 characterized in that 90 % of the particle size of the docosanoic acid glyceryl ester ranges from 1.5 to 60 micrometers.
4. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claims 2 and 3 characterized in that the contents of the higher fatty acids glyceryl esters is in the range of from 10 to 53 % by weight, preferably from 28 to 47 % by weight.
5. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claims 1 and 2 characterized in that it contains alkali salts of phosphoric acid, preferably calcium phosphate dihydrate in an amount from 20 to 41 % by weight.
6. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 5 characterized in that it contains calcium phosphate dihydrate preferably in an amount from 24 to 39 % by weight.
7. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claims 1 , 2 and 5 characterized in that it contains non-ionic vinylpyrrolidone polymers having a relative molecular weight of 9000 to 90,000 in an amount of 1.15 to 1.75 % by weight.
8. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 7 characterized in that it contains non- ionic vinylpyrrolidone polymers having a relative molecular weight of preferably 25,000 to 30,000 in amount of preferably from 1.3 to 1.55 % by weight.
9. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claims 1 , 2, 5 and 7 characterized in that it contains substances from the group salts of higher fatty acids with alkaline earth metals in an amount of 1.5 to 3.2 % by weight.
10. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 9 characterized in that it contains substances from the group salts of higher fatty acids with alkaline earth metals, preferably magnesium stearate in an amount of preferably from 1.8 to 2.8 % by weight.
11. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claims 1 , 2, 5, 7 and 9 characterized in that it contains silicon oxides in an amount of 1 to 3.0 % by weight.
12. The controlled release pharmaceutical composition containing tramadol hydrochloride according to claim 1 1 characterized in that it contains silicon oxides, preferably colloidal silica in an amount of 1.1 to 2.1 % by weight.
13. A method of preparing the pharmaceutical composition according to claims 1 to 12 characterized in that the active ingredient is agitated in admixture with micronized esters of glycerol with higher fatty acids and alkali salts of phosphoric acid wherein said admixture is moisturized with a solution of a non-ionic vinylpyrrolidone polymer in a mixture of water and ethyl alcohol and the mixture is agglomerated.
14. The method of preparing the pharmaceutical composition according to claim 13 characterized in that the active ingredient is agitated in admixture with micronized esters of glycerol with higher fatty acids, preferably glyceryl ester of docosanoic acid of a particle size from 1 to 100 μm, preferably 1.5 to 60 μm, in an amount of 10 to 53 % by weight, preferably 28 to 47 % by weight, along with alkali salts of phosphoric acid, preferably calcium phosphate dihydrate, in an amount of 20 to 41 % by weight, preferably of 24 to 39 % by weight.
15. The method of preparing the pharmaceutical composition according to claims 13 and 14 characterized in that the mixture of the active ingredient, esters of glycerol with higher fatty acids and alkali salts of phosphoric acid is moisturized with a solution of a non-ionic vinylpyrrolidone polymer of a relative molecular weight from 9000 to 90,000, preferably 25,000 to 30,000, in an amount of 1.15 to 1.75 % by weight, preferably 1.3 to 1.55 % by weight.
16. The method of preparing the pharmaceutical composition according to claims 13 to 15 characterized in that the mixture of the active ingredient, esters of glycerol with higher fatty acids and alkali salts of phosphoric acid is moisturized with a solution of a non-ionic vinylpyrrolidone polymer in a mixture of water and ethyl alcohol in an amount of 30 to 70 % by weight, preferably 40 to 60 % by weight.
17. The method of preparing the pharmaceutical composition according to claims 13 to 16 characterized in that the mixture is agitated and agglomerated, the obtained agglomerate being dried in a suitable manner by fluidising drying, chamber drying or vacuum drying such that the mixture contains from 0.2 to 1.5, preferably from 0.5 to 1.2 % moisture.
18. The method of preparing the pharmaceutical composition according to claims 13 to 17 characterized in that the dried agglomerate is adjusted to a particle size convenient for tabletting process and substances from the group of salts of higher fatty acids with alkaline earth metals and/or silicon oxides are admixed, the mixture being agitated until homogeneous.
19. The method of preparing the pharmaceutical composition according to claim 18 characterized in that the dried agglomerate is adjusted to a particle size convenient for tabletting process and admixed are substances from the group of salts of higher fatty acids with alkaline earth metals, preferably magnesium stearate in an amount of 1.5 to 3.2 % by weight, preferably 1.8 to 2.8 % by weight, and/or silicon oxides, preferably colloidal silica in an amount froml to 3 % by weight, preferably from 1.1 to 2.1 % by weight.
20. The method of preparing the pharmaceutical composition according to claims 13 to 19 characterized in that the prepared mixture is tabletted to tablets having a lenticular, flat oblong or other shapes such that break resistance of the tablets ranges between 40 and 110 N, preferably from 50 to 90 N.
EP00987947A 1999-12-28 2000-12-20 Controlled release pharmaceutical composition containing tramadol hydrochloride Expired - Lifetime EP1255535B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SI200030873T SI1255535T1 (en) 1999-12-28 2000-12-20 Controlled release pharmaceutical composition containing tramadol hydrochloride

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
SK1868-99A SK285128B6 (en) 1999-12-28 1999-12-28 A remedy with controlled release comprising tramadol hydrochloride and method for preparation thereof
SK186899 1999-12-28
PCT/SK2000/000027 WO2001047497A2 (en) 1999-12-28 2000-12-20 Controlled release pharmaceutical composition containing tramadol hydrochloride

Publications (2)

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EP1255535A2 true EP1255535A2 (en) 2002-11-13
EP1255535B1 EP1255535B1 (en) 2006-04-26

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US (1) US20030175343A1 (en)
EP (1) EP1255535B1 (en)
JP (1) JP2003518486A (en)
AT (1) ATE324103T1 (en)
AU (1) AU2421601A (en)
BG (1) BG65713B1 (en)
CA (1) CA2397942C (en)
CY (1) CY1106127T1 (en)
CZ (1) CZ297394B6 (en)
DE (1) DE60027601T2 (en)
DK (1) DK1255535T3 (en)
EA (1) EA006438B1 (en)
EE (1) EE05231B1 (en)
ES (1) ES2266018T3 (en)
GE (1) GEP20053532B (en)
HU (1) HUP0203842A3 (en)
LT (1) LT5033B (en)
LV (1) LV12917B (en)
PL (1) PL208096B1 (en)
PT (1) PT1255535E (en)
SI (1) SI1255535T1 (en)
SK (1) SK285128B6 (en)
TW (1) TWI221419B (en)
UA (1) UA76411C2 (en)
WO (1) WO2001047497A2 (en)

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US8128957B1 (en) 2002-02-21 2012-03-06 Valeant International (Barbados) Srl Modified release compositions of at least one form of tramadol
US20050182056A9 (en) * 2002-02-21 2005-08-18 Seth Pawan Modified release formulations of at least one form of tramadol
SK286107B6 (en) * 2002-04-12 2008-03-05 Zentiva, A. S. Analgesically active peroral therapeutic composition with controlled release of an opioid active substance and method for the preparation thereof
DE10245623A1 (en) * 2002-09-30 2004-04-08 Clariant Gmbh Esters and partial esters from polyhydric alcohols
PL1651248T3 (en) * 2003-07-11 2010-02-26 Novartis Ag Orally dosed pharmaceutical compositions comprising a delivery agent in micronized form
US20080274264A1 (en) * 2006-06-09 2008-11-06 John Godber Calcium fortification substance for clear beverages
US20100143573A1 (en) * 2006-06-09 2010-06-10 John Godber Mineral fortification substance for clear beverages
DE102006044694A1 (en) * 2006-09-22 2008-03-27 Krewel Meuselbach Gmbh Peroral solid analgesic preparation
US20100003322A1 (en) * 2008-07-03 2010-01-07 Lai Felix S Enteric coated hydrophobic matrix formulation
HUE051406T2 (en) 2012-11-14 2021-03-01 Grace W R & Co Compositions containing a biologically active material and a non-ordered inorganic oxide

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IL109460A (en) 1993-05-10 1998-03-10 Euro Celtique Sa Controlled release formulation comprising tramadol
DE4329794C2 (en) * 1993-09-03 1997-09-18 Gruenenthal Gmbh Tramadol salt-containing drugs with delayed release
EP0654263B1 (en) 1993-11-23 2002-01-23 Euro-Celtique S.A. Method for preparing a sustained release composition
DE4343993A1 (en) * 1993-12-22 1995-06-29 Stockhausen Chem Fab Gmbh Graft copolymers of unsaturated monomers and polyhydroxy compounds, process for their preparation and their use
FR2753904B1 (en) * 1996-10-01 1998-10-30 Gattefosse Ets Sa PHARMACEUTICAL COMPOSITION WITH MODIFIED RELEASE OF ACTIVE SUBSTANCE, INCLUDING A MATRIX, AND MANUFACTURING PROCESS
US5980941A (en) * 1997-08-20 1999-11-09 Fuisz Technologies Ltd. Self-binding shearform compositions
DE19901683B4 (en) * 1999-01-18 2005-07-21 Grünenthal GmbH Controlled-release analgesic
US6248363B1 (en) * 1999-11-23 2001-06-19 Lipocine, Inc. Solid carriers for improved delivery of active ingredients in pharmaceutical compositions

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO0147497A2 *

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CA2397942A1 (en) 2001-07-05
BG106952A (en) 2003-03-31
ATE324103T1 (en) 2006-05-15
ES2266018T3 (en) 2007-03-01
HUP0203842A3 (en) 2004-06-28
BG65713B1 (en) 2009-08-31
WO2001047497A3 (en) 2002-09-12
EA200200720A1 (en) 2003-02-27
EE05231B1 (en) 2009-12-15
HUP0203842A2 (en) 2003-05-28
AU2421601A (en) 2001-07-09
SI1255535T1 (en) 2006-10-31
SK186899A3 (en) 2001-07-10
PT1255535E (en) 2006-09-29
CY1106127T1 (en) 2011-06-08
UA76411C2 (en) 2006-08-15
GEP20053532B (en) 2005-05-25
DK1255535T3 (en) 2006-08-28
JP2003518486A (en) 2003-06-10
EE200200368A (en) 2003-10-15
CZ20022371A3 (en) 2002-10-16
LV12917B (en) 2003-02-20
DE60027601T2 (en) 2007-04-26
PL208096B1 (en) 2011-03-31
PL357680A1 (en) 2004-07-26
LT2002078A (en) 2003-03-25
SK285128B6 (en) 2006-07-07
TWI221419B (en) 2004-10-01
DE60027601D1 (en) 2006-06-01
WO2001047497A2 (en) 2001-07-05
EP1255535B1 (en) 2006-04-26
EA006438B1 (en) 2005-12-29
CA2397942C (en) 2008-07-15
US20030175343A1 (en) 2003-09-18
CZ297394B6 (en) 2006-12-13
LT5033B (en) 2003-07-25

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